Soneerawater

Treatment system overview

• Continuous flow system using electrolysis

– Filter and membrane free

– No added chemicals, reagents, flocculants or clarifiers

• Removes the widest array of contaminants

• Power saving up to 80%

• Opex cost saving up to 80%

• A 40’ container can treat up to 0.2MGD

Technology overview: How the process works

Effluent Enters Clean water in end chamber

Chemical reactions occur in middle chambers

Technical Aspects

• Uses a bubble – ion barrier to remove pollutants

• Pollutants automatically removed during operation

• Removes most pollutants better than DAF

• Removal rates typically 95% to 98%

• Power usage depends upon pollutant loading, typically 0.3 to 0.7kWh/m3

• Fast throughput, typically 1hr from polluted to cleaned water

• Fully scalable

Treatment Capability

Process Results

1. Oil & petroleum in stagnant water with algae treated in 60 minutes

2. Raw sewage treated within 45 minutes

Removal Rates

Material Raw

mg/L

Cleaned

mg/l % Removal

Faecal Coliforms 72,000,000 1300 (est) 99.9

E. coli 1,800,000 9,000 99.5

BOD5 102.60 4.5 95.6

COD 145,500 5,320 96.3

Total Kjeldahl Nitrogen 81 46 43.2

Total Nitrogen 48 34 29.2

Nitrate 4.20 0.20 95.2

Ammonia-N 0.24 <0.03 >88.9

Oxidised-N 0.20 <0.1 >50

TOC 6,091 36.8 99.40

TSS 1,900 19 99.00

Colour 24.20 <1 >95.9

Turbidity >2000 20 >99

Oil & Grease 81,440 20 99.98

Grease 150 <3 >98

Petroleum Hydrocarbons 1,200 15 98.8

Ethanol 9.30 <0.05 >99.5

Acetone 0.69 <0.05 >94.2

Benzene 0.12 <0.001 >99.2

Toluene 0.99 <0.001 >99.9

Ethyl Benzene 2.1 <0.005 >99.8

Xylenes 4.8 <0.005 >99.9

TRH C6-C9 8.7 0.002 >99.8

TRH C10-C14 9.1 2.6 71.4

Aluminium 16 0.66 95.9

Arsenic 0.73 0.01 98.6

Barium 5.6 0.13 97.7

Boron 0.42 0.17 59.5

Cadmium 0.049 <0.001 >98

Calcium 36 16 55.6

Cobalt 0.06 0.01 83.3

Copper 260 0.27 99.9

Dissolved Oxygen 0.26 8.9 X 35 increase

Iron 1.009 0.014 98.7

Lead 5.4 <0.01 >99.8

Magnesium 5.6 2.5 55.4

Manganese 0.28 <0.01 >96.4

Nickel 0.02 0.003 85

Phosphorus 27.5 0.4 98.5

Selenium 0.04 0.01 75

Tin 0.85 <0.01 >98.8

Titanium 1.1 <0.01 >99.1

Vanadium 0.8 <0.01 >87.5

Zinc 180 0.42 99.8

Arizona-based Operational System

Treating raw sewage at Surprise WWTP

Floating the contaminants

Removing the waste (Click picture & press play at bottom right)

Treatment results in Phoenix

Raw sewage & trade waste (press play)

Small footprint - 125,000 GPD

Skid Mounted – highly mobile

Unique Features

• No filters to clog; No chemicals to pollute

• 98% of contaminants removed

• Very low energy use - typically 20kW for 275,000 GPD

• Can be solar powered

• Automated process with Remote monitoring

• Scalable from 10,000G/D to over 10MG/D

• Complements other water treatment processes

• Very small footprint – 0.2MGD fits into a shipping container

• Less than 5% of the water is removed with the waste

• The waste is inert, non leachable; suitable for landfill or fertilizer

• Highly suitable system for environmentally sensitive sites

Australian Systems

1. Operational mine site in Sydney. Tasked to clean stormwater and mining effluent before it enters the National Park and drinking water catchment. Delivering 350,000gal/day

2. Small 20’ system at the Adelaide sewage plant

3. Other sites include: a. Providing drinking water in National parksb. Providing drinking water in two State prisonsc. Providing drinking water in a large seasonal caravan parkd. Cleaning ballast water from a Sydney Marinae. Recycling water used to clean council garbage trucksf. Providing primary and secondary treatment for a food manufacturer

Points of Contact

Glen Marshall Michael StevensCEO VP Manufacturing & OperationsPh: +1 480 570 1852 Ph: +1 480 319 3558E: glen@Soneerawater.com E: mick@Soneerawater.com

Darrell BehanCOOPh: +1 480 570 2703E: darrell@Soneerawater.com